CN1104284C - ERS-10 zeolite and process for its preparation - Google Patents

ERS-10 zeolite and process for its preparation Download PDF

Info

Publication number
CN1104284C
CN1104284C CN97103349A CN97103349A CN1104284C CN 1104284 C CN1104284 C CN 1104284C CN 97103349 A CN97103349 A CN 97103349A CN 97103349 A CN97103349 A CN 97103349A CN 1104284 C CN1104284 C CN 1104284C
Authority
CN
China
Prior art keywords
sio
compound
crystalline material
ers
formula
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN97103349A
Other languages
Chinese (zh)
Other versions
CN1164439A (en
Inventor
L·卡卢西奥
R·米利尼
G·贝卢西
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Eni Tecnologie SpA
Original Assignee
Eniricerche SpA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Eniricerche SpA filed Critical Eniricerche SpA
Publication of CN1164439A publication Critical patent/CN1164439A/en
Application granted granted Critical
Publication of CN1104284C publication Critical patent/CN1104284C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/04Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B39/00Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
    • C01B39/02Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
    • C01B39/46Other types characterised by their X-ray diffraction pattern and their defined composition
    • C01B39/48Other types characterised by their X-ray diffraction pattern and their defined composition using at least one organic template directing agent

Abstract

A novel porous crystalline material, designated ERS-10 zeolite, is described, having in its calcined and anhydrous form a molar composition of oxides corresponding to the formula (I) mM2/nO.zX2O3.YO2 wherein: m is a number between 0.01 and 10, M is H<+> and/or a cation of an alkaline or earth-alkaline metal with valence n, z is a number between 0 and 0.02, X represents one or more elements selected from aluminum, iron, gallium, boron, vanadium, arsenic, antimonium, chromium and manganese and Y represents one or more elements selected from silicon, germanium, titanium, zirconium, characterized by an X-ray diffraction spectrum of the powders shown in table 1. A process is also described for the preparation and purpose of this material.

Description

ERS-10 zeolite and preparation method thereof
The present invention relates to a kind of novel porous crystalline material, ERS-10 zeolite hereinafter referred to as, and relate to a kind of azo spirocyclic compound with general formula (II) expression prepares this zeolite as organic formwork agent method.
The invention still further relates to this material as the application of catalyzer in hydrocarbon conversion process, as the application of molecular sieve and ion-exchanger.
The zeolite in natural origin and synthetic source is the silico-aluminate that the porous crystalline characteristic is arranged, and it is by TO 4Tetrahedral three-dimensional network is formed, and wherein T can be silicon or aluminium.Existing of trivalent aluminium with tetrahedral coordination in crystal lattice produces excessive negative charge, and it is by basic metal (Na, K, Rb, Li and Cs) ion, alkaline-earth metal (Mg and Ca) ion, organic ammonium positively charged ion or hydrogen ion balance.
It is that known zeolite facies exist that mass crystallization structure major part is arranged.The feature of each zeolite facies is to exist with well-regulated and definite size to be in the special hole that the duct and/or the cage of 3~15 dusts are represented.On the basis of the mean sizes in hole, usually zeolite is divided into " aperture ", " mesopore " and " macropore " zeolite.These features make zeolite be applicable to various fields, as the separation of ion-exchange, gas or liquid mixture, perhaps are used as catalyzer in various hydrocarbon conversion reactions.
Zeolite reacts under hydrothermal condition by the reaction mixture that contains silicon source, aluminium source, organic formwork agent and optional basic metal or alkaline earth salt usually and prepares.Under the condition that is fit to, template plays a part the zeolite synthesis fixed structure that leads, and it is selected from amine and organic quaternary ammonium salt or phosphonium salt usually.
The characteristic of the zeolite that makes depends on the character of composition, reaction conditions and the particularly used organic formwork agent of reaction mixture.
For example, with tetraethyl ammonium hydroxide (Et 4When NOH) making template, make β zeolite (US.3308069), and with TPAOH (n-Pr 4When NOH) making template, make ZSM-5 zeolite (U.S.3702886).In some cases, available identical organic formwork agent but synthesize the zeolite (US 4016245, EP-293032, US 4052472) that different structure is arranged with different synthesis conditions.
Have now found that,, use the azo spirocyclic compound of general formula (II) can make novel porous crystalline material as organic formwork agent according to the present invention, ERS-10 zeolite hereinafter referred to as, it is active in catalysis.
In view of the above, the present invention relates to a kind of like this porous crystalline material ERS-10, the anhydrous form of its roasting has the oxide molar of following formula (I) to form:
MM 2/nOzX 2O 3YO 2(I) in the formula, m is the number between 0.01~10, and M is H +And/or valence mumber is alkali metal cation or the alkaline earth metal cation of n, z is the number between 0~0.02, X represents to be selected from one or more elements of aluminium, iron, gallium, boron, vanadium, arsenic, antimony, chromium and manganese, and Y represents to be selected from one or more elements of silicon, germanium, titanium, zirconium.
X is the aluminium that replaced by a kind of element of chosen from Fe, gallium, boron, vanadium, arsenic, antimony, chromium and manganese of aluminium or part preferably, and the silicon that a kind of element of Y to be silicon or part be selected from germanium, titanium, zirconium replaces.
The ERS-10 zeolite of calcined form characterizes with X-ray powder diffraction figure, writes down diffractogram with the vertical side angle meter of charged subpulse counter system, uses CuK ray (λ=1.54178 dusts), and its principal reflection peak is shown in table 1 and Fig. 1.
Table 1d () I/I 010011.0±0.1 vs6.80±0.08 w5.79±0.06 w4.59±0.05 m4.29±0.05 vs3.96±0.04 m3.69±0.03 w3.41±0.03 w3.33±0.03 w3.26±0.02 m3.07±0.02 w2.68±0.01 w2.57±0.01 w2.51±0.01 w2.38±0.01 w2.31±0.01 w2.28±0.01 w2.11±0.01 w2.03±0.01 w1.94±0.01 w
Wherein, d presentation surface spacing, I/I 0The relative intensity of 100 expressions to represent with respect to the percentage ratio of the peak height of the height of highest peak, symbol vs represents very strong intensity (60-100), and s represents strong intensity (40~60), and m represents medium intensity (20~40), and w represents weak intensity (0-20).
The total pore volume of ERS-10 zeolite is 0.13~0.19 a milliliter/gram, and surface-area is about 350 meters 2/ gram.
The Philips EM400T transmission electron microscope (TEM) that use is worked under 120 kiloelectron volts, and use controlled electron beam intensity, with the infringement that prevents that material is possible, it might obtain the image with respect to ERS-10 zeolitic material porous crystalline structure.At first sample is enclosed in the Resins, epoxy, after the sclerosis, the ultramicrotome cutting with diamond blade is housed obtains the thin slice that thickness is 300~700 dusts.Then identical thin slice is deposited on the copper grid, image accumulates on the crystal that is suspended on the grate opening, to avoid overlapping with support.
Fig. 3 represents the Photomicrograph of ERS-10 crystallization aggregate, might obtain the direct visible image of zeolitic material vesicular structure from this figure.Particularly, this structure is determined in the zone that A represents in Fig. 3 Photomicrograph well, and in the figure (Fig. 4) that amplifies relatively, arrange by oblique bi-directional pattern at hole (light color place).Because the resolving power limited (point resolution 3.7 dusts) of used TEM instrument can not record the size in hole exactly.
ERS-10 zeolite of the present invention can make with a kind of like this method, and this method comprises:
(a) preparation optional containing at least aly can be hydrolyzed into X 2O 3Compound, at least aly can be hydrolyzed into YO 2Compound, basic metal or alkaline earth metal cation source or the aqueous solution of its mixture and organic formwork agent (Q), it is characterized in that described template is the azo spirocyclic compound of general formula (II).
Figure C9710334900101
In the formula, n and n ' are identical or different, an integer in the expression 3~6, X -For being selected from OH -, muriate, bromide, fluorochemical and iodide a kind of negatively charged ion, wherein the quantity of each reagent obtains following mol ratio:
YO 2/X 2O 3 50/1~∞
OH -/YO 2 0.15/1~0.7/1
Q/YO 2 0.1/1~0.5/1
H 2O/YO 2 20/1~60/1
M +/YO 2 0.05/1~0.20/1
The solution that obtains in (a) is remained under the sufficient reaction conditions, generate the solid crystal material;
(c) drying solid crystalline material, its anhydrous form have the oxide molar of general formula (III) to form,
YQ 2OmM 2/nOzX 2O 3YO 2(III) in the formula, y is a numerical value between 0.1~1, and Q is for there being the organic formwork agent of general formula (II), and M is the positively charged ion of basic metal and/or alkaline-earth metal, and m, n, z, X and Y have the as above implication of regulation;
(d) crystalline material of the formula (III) that in step (c), obtains of roasting; And
(e) use H +To small part replacement positively charged ion M, obtain the acid type ERS-10 zeolite of formula (I).
When X be aluminium or part replace aluminium the time, the compound that can be used in the step a) of the inventive method is selected from aluminium isopropylate, Tai-Ace S 150, NaAlO 2Aluminium isopropylate and Tai-Ace S 150 are preferred.
When Y was the silicon of silicon or part replacement, compound can be selected from tetraethyl orthosilicate (TES), colloidal silica (LUDOX ), water glass, silicon oxide (AEROSIL ignites ).TES and LUDOX Be preferred.
In the step (a) of the inventive method, sodium hydroxide or potassium hydroxide are preferably used as cationic source.
As organic formwork agent (Q), preferably use the compound of formula (II), wherein n is identical with n ', its value equals 5, X -Be OH -
In step (a), the adding order of each component of solution is inessential.But, preferably at first make and contain that organic template is optional at least aly to be hydrolyzed into X 2O 3Compound and the aqueous solution of cationic source, can be hydrolyzed into YO with at least a then 2Compound join in this solution.
Under any circumstance, following mol ratio is arranged in the solution that generates:
YO 2/X 2O 3 50/1~∞
OH -/YO 2 0.15/1~0.7/1
Q/YO 2 0.1/1~0.5/1
H 2O/YO 2 20/1~60/1
M +/YO 2 0.05/1~0.20/1
Preferred ratio is:
YO 2/X 2O 3 80/1~∞
OH -/YO 2 0.2/1~0.45/1
Q/YO 2 0.2/1~0.3/1
H 2O/YO 2 40/1~50/1
M +/YO 2 0.09/1~0.15/1
In the step (b) of the inventive method,, preferably about 170 ℃, carry out crystallization at 150~180 ℃.
Reaction times and temperature of reaction, concentration are relevant with other factors, are generally 3~28 days, preferred 7~14 days.Reaction is carried out under autogenous pressure usually, preferably under agitation carries out.
When reaction finishes, as filtering, from mother liquor, isolate the solid crystal phase with conventional technology, with the softening water washing, and in the step (c) of the inventive method, carry out drying.
Drying should be no more than about 170 ℃, carries out such for some time under preferred about 90~120 ℃, during this period of time is enough to fully or almost completely remove moisture.
After drying, there is the crystalline material of general formula (III) that the X-ray diffractogram of measuring is as mentioned above arranged, it has the principal reflection peak among table 2 and Fig. 2.
Table 2d () I/I 010011.1±0.1 s6.82±0.08 w5.83±0.06 w4.64±0.05 m4.32±0.05 vs4.00±0.04 s3.72±0.03 m3.42±0.03 w3.35±0.03 w3.27±0.02 m3.08±0.02 w2.70±0.01 w2.58±0.01 w2.54±0.01 w2.39±0.01 w2.32±0.01 w2.29±0.01 w2.12±0.01 w2.11±0.01 w1.94±0.01 w
In the step (d) of the inventive method, the crystalline material of formula (III) is carried out roasting, so that remove the organic formwork agent of occlusion in porous system.This processing is carried out in oxidizing atmosphere usually, for example carries out in air.Maturing temperature in 500~700 ℃ of scopes, preferred 550~650 ℃.Roasting time can change to 20 hours from 4 hours, about 6~15 hours usually.
In the step (e) of the inventive method, usable acid is mineral acid particularly, example hydrochloric acid or with ammonium salt such as ammonium acetate ion-exchange, and then the method for roasting realizes using H +To small part replacement positively charged ion M.
Particularly, can make the zeolite of ammonia type exchange by following three partially disposed: under magnetic stirs, handling 1 hour under 80 ℃ with ammonium acetate solution; Finish the after-filtration product, repeat to wash with softening water; Drying and roasting under these conditions.
X-ray powder diffraction figure through the acid type ERS-10 of roasting zeolite is similar to shown in the table 1.
If desired, methods such as available extrusion are carried out forming processes with catalyzer, make solid be transformed into the required physical form of final application.
In fact, the pattern of visual response device and deciding, ERS-10 zeolitic material of the present invention can use the microsphere particle or the bead of different shapes and pattern.
The ERS-10 catalyzer of acid type of the present invention is active in the chemical reaction that needs the acid catalysis effect, for example in hydrocarbon conversion reactions, as cracking, isomerization, oligomerisation, alkylation, hydrotreatment etc.ERS-10 catalyzer of the present invention also can be used as ion-exchanger and molecular sieve.
The sole purpose of following examples is to illustrate in greater detail the present invention, and never should regard following examples as limitation of the scope of the invention.
Embodiment 1
Under agitation 10.4 gram tetraethyl orthosilicates are added in the solution that contains 45 gram softening waters, 0.204 gram aluminium isopropylate, 0.19 gram sodium hydroxide and 1.71 gram 6-nitrogen spiral shell-[5,5]-undecane oxyhydroxide (Q).These operations are at room temperature carried out.When hydrolysis is complete, obtain the milky white solution of forming by following mol ratio:
SiO 2/Al 2O 3=100/1
Na +/SiO 2=0.095/1
Q/SiO 2=0.2/1
H 2O/SiO 2=50/1
OH -/SiO 2=0.295
In the steel autoclave of then solution being packed into, put into stove and under 170 ℃, autogenous pressure, kept 14 days.Behind the cool to room temperature, from mother liquor, isolate crystallized product with filtering method, with softening water washing, and in stove 120 ℃ dry 2 hours down.
The crystalline material of measuring with the element chemical analysis method composed as follows:
67SiO 2∶1Al 2O 3∶0.5Q 2O∶0.3Na 2O∶7H 2O
Carry out the X-ray powder diffraction analysis with the vertical goniometer (Phillips) that electronic impulse counting system is housed, use CuK ray (λ=1.54178 dusts).The spectrogram of this sample is shown in table 3.
Table 3
d() 100.I/I 0 11.9±0.10 41 6.82±0.08 3 5.83±0.06 2 4.64±0.05 39 4.32±0.05 100 4.00±0.04 46 3.72±0.03 21 3.42±0.03 12 3.35±0.03 17 3.27±0.02 40 3.08±0.02 4 2.70±0.01 5 2.58±0.01 2 2.54±0.01 4 2.39±0.01 22.32±0.01 32.29±0.01 32.12±0.01 22.11±0.01 32.03±0.01 12.00±0.01 21.94±0.01 41.91±0.01 31.87±0.01 21.85±0.01 1
Then in airflow, with crystallized sample 550 ℃ of roastings 5 hours.Chemical analysis obtains following composition:
67SiO 2∶1Al 2O 3∶0.3Na 2O
Use ammonium acetate solution 80 ℃ of following re-treatments the product of roasting then, with the softening water washing and 550 ℃ of following roastings 5 hours, so that be exchanged into acid type.
The X-ray powder diffraction spectrogram of this acid type sample is shown in table 4.
Table 4d () I/I 010010.97±0.10 1006.79±0.08 125.79±0.06 84.59±0.05 474.29±0.05 793.96±0.04 393.69±0.03 173.41±0.03 93.33±0.03 163.26±0.02 373.07±0.02 42.68±0.01 42.57±0.01 12.50±0.01 72.38±0.01 32.31±0.01 22.28±0.01 22.11±0.01 32.03±0.01 11.99±0.01 11.94±0.01 21.90±0.01 2
Measure the existence that confirms lewis' acid and bronsted acid with pyridine as the acidity that the test molecule carries out.
Embodiment 2
Adopt the step identical, use 0.408 to restrain aluminium isopropylate with embodiment 1.When hydrolysis finishes, obtain the milky white solution of forming by following mol ratio:
SiO 2/Al 2O 3=50/1
Na +/SiO 2=0.0475/1
Q/SiO 2=0.2/1
H 2O/SiO 2=45/1
OH -/SiO 2=0.2475/1
X-ray diffractogram after drying and the roasting is the spectrogram shown in the similar table 3 and 4 respectively.
Embodiment 3
With 0.315 gram Al 2(SO 4) 316H 2O and 10 gram Ludox AS (30%) is added in the solution that contains 33.5 gram softening waters, 0.19 gram sodium hydroxide and 1.71 gram 6-nitrogen spiral shell-[5,5]-undecane oxyhydroxide.
After hydrolysis fully, make the shallow milky white solution of forming by following mol ratio:
SiO 2/Al 2O 3=100/1
Na +/SiO 2=0.095/1
Q/SiO 2=0.2/1
H 2O/SiO 2=45/1
OH/SiO 2=0.295/1
The steel autoclave of then solution being packed into is put into stove and was kept 14 days under 170 ℃, autogenous pressure.Behind the cool to room temperature, from mother liquor, isolate crystallized product with filtration method, with softening water washing, in 120 ℃ of stoves dry 2 hours then.
The X-ray powder diffraction data of this sample are listed table 3 in.
Roasting is after 5 hours in 550 ℃, air, be exchanged into acid type with ammonium acetate solution 80 ℃ of following re-treatments, 120 ℃ down dry, roasting 5 hours in 550 ℃ of following air then, obtain pure ERS-10 zeolite facies, characterize fully and that table 4 is listed is similar with X-ray powder diffraction.
Embodiment 4
Adopt the step identical, use 0.173 gram aluminium isopropylate and 10.4 to restrain tetraethyl orthosilicates with embodiment 1.
Hydrolysis obtains the shallow milky white solution of being made up of following mol ratio after finishing:
SiO 2/Al 2O 3=120/1
Na +/SiO 2=0.095/1
Q/SiO 2=0.2/1
H 2O/SiO 2=45/1
OH/SiO 2=0.295/1
After the dry and roasting, this material has respectively and table 3 and 4 listed identical X-ray powder diffraction data.
Embodiment 5
Adopt the step identical, use 0.128 gram aluminium isopropylate and 10.4 to restrain tetraethyl orthosilicates with embodiment 1.
Hydrolysis obtains the shallow milky white solution of being made up of following mol ratio after finishing:
SiO 2/Al 2O 3=160/1
Na +/SiO 2=0.095/1
Q/SiO 2=0.2/1
H 2O/SiO 2=45/1
OH/SiO 2=0.295/1
After the dry and roasting, the X-ray powder diffraction data respectively with table 3 and 4 listed identical.
Embodiment 6
10.4 gram tetraethyl orthosilicates are added in the solution that contains 45 gram softening waters, 0.19 gram sodium hydroxide and 1.71 gram 6-nitrogen spiral shell-[5,5]-undecane oxyhydroxide.
After hydrolysis fully, make the clear solution of forming by following mol ratio.
SiO 2/Al 2O 3=x
Na +/SiO 2=0.095/1
Q/SiO 2=0.2/1
H 2O/SiO 2=50/1
OH/SiO 2=0.295/1
The steel autoclave of then solution being packed into is put into stove, keeps 7 days under 170 ℃, autogenous pressure.Behind the cool to room temperature, from mother liquor, isolate crystallized product with filtration method, with the softening water washing, following dry 2 hours at 120 ℃ then.The main X-ray powder diffraction data of this sample are listed table 3 in.
Roasting obtained pure ERS-10 zeolite facies after 5 hours in 550 ℃ of following air, characterized the listed result of all fours table 4 with X-ray powder diffraction.
Embodiment 7 (contrast)
15.6 gram tetraethyl orthosilicates are added to contain 27 gram softening waters, 0.306 gram aluminium isopropylate and 3.85 gram 6-nitrogen spiral shell-[5,5]-undecane oxyhydroxide.When hydrolysis is complete, obtain the complete clear solution of forming by following mol ratio:
SiO 2/Al 2O 3=100/1
Q/SiO 2=0.3/1
H 2O/SiO 2=20/1
With the solution steel autoclave of packing into, put into stove, under 170 ℃, autogenous pressure, kept 14 days.Behind the cool to room temperature, from mother liquor, isolate crystallized product with filtration method, with the softening water washing, following dry 2 hours at 120 ℃ then.X-ray powder diffraction figure shows has ZSM-12 zeolite facies (MTW) to exist.
This result shows that the existence of sodium is necessary for making the ERS-10 zeolite.
Embodiment 8 (contrast)
10.4 gram tetraethyl orthosilicates are added in the solution that contains 40.5 gram softening waters, 0.68 gram aluminium isopropylate, 0.62 gram sodium hydroxide and 1.71 gram 6-nitrogen spiral shell-[5,5]-undecane oxyhydroxide.
When hydrolysis is complete, obtain the white suspension of the homogeneous formed by following mol ratio:
SiO 2/Al 2O 3=30/1
Na +/SiO 2=0.31/1
Q/SiO 2=0.2/1
H 2O/SiO 2=45/1
OH/SiO 2=0.51/1
Solution is packed in the steel autoclave, put into stove, and under 170 ℃, autogenous pressure, placed 14 days.Behind the cool to room temperature, from mother liquor, isolate crystallized product with filtration method, with the softening water washing, following dry 2 hours at 120 ℃ then.X-ray powder diffraction figure shows mordenite is arranged (MOR) exists.
Embodiment 9
The material through roasting that obtains among the embodiment 1 can be used as molecular sieve.Use NH 3, normal hexane, hexanaphthene and sym-trimethylbenzene adsorb measurement as the test molecule.These measurements are carried out according to the following steps:
-with powder at 500 ℃, 6 * 10 -5The millibar decompression activates 1 hour down;
-under 23 ℃, identical vacuum tightness, system was stablized 16 hours;
-add test molecular vapors in a small amount down at 23 ℃, until balance;
-with testing the known coefficient of expansion of molecule and balance piezometry adsorptive capacity.
Be shown in table 5 with the loading capacity that the gram adsorbed product/100 gram catalyzer are represented.
Table 5
The test molecule Size (dust) Adsorptive capacity (gram/100 gram ERS-10)
NH 3 2.6 2.35
n-C 6H 14 4.3 3.10
C 6H 12 6.0 2.15
Sym-trimethylbenzene 8.1 0.45
*Equilibrium pressure is 0.6 millibar

Claims (20)

1. porous crystalline material that is called the ERS-10 zeolite, this material has the oxide molar of general formula (I) to form through the anhydrous form of roasting:
MM 2/nOzX 2O 3YO 2(I) in the formula, m is the number in 0.01~10, and M is H +And/or valence mumber is alkali metal cation or the alkaline earth metal cation of n, z is the number in 0~0.02, X represents to be selected from one or more elements of aluminium, iron, gallium, boron, vanadium, arsenic, antimony, chromium and manganese, Y represents to be selected from one or more elements of silicon, germanium, titanium, zirconium, and this material characterizes with the X-ray powder diffraction figure shown in the following table 1:
Table 1d () I/I 010011.0±0.1 vs6.80±0.08 w5.79±0.06 w4.59±0.05 m4.29±0.05 vs3.96±0.04 m3.69±0.03 w3.41±0.03 w3.33±0.03 w3.26±0.02 m3.07±0.02 w2.68±0.01 w2.57±0.01 w2.51±0.01 w2.38±0.01 w2.31±0.01 w2.28±0.01 w2.11±0.01 w2.03±0.01 w1.94±0.01 w
2. according to the porous crystalline material of claim 1, wherein M is selected from sodium, potassium, hydrogen or its mixture.
3. according to the porous crystalline material of claim 1, wherein X is aluminium or the aluminium that partly replaced by the element of chosen from Fe, gallium, boron vanadium, arsenic, antimony, chromium and manganese.
4. according to the porous crystalline material of claim 1, wherein Y is the silicon that silicon or the element that is selected from germanium, titanium and zirconium partly replace.
5. method for preparing the porous crystalline material ERS-10 of claim 1, this method comprises:
(a) preparation optional containing at least aly can be hydrolyzed into X 2O 3Compound, at least aly can be hydrolyzed into YO 2The cationic source of compound, basic metal or alkaline-earth metal and the aqueous solution of a kind of organic formwork agent (Q), it is characterized in that described template is the azo spirocyclic compound that general formula (II) is arranged In the formula, n and n ' are identical or different, an integer in the expression 3~6, X -For being selected from OH -, muriate, bromide, fluorochemical and iodide negatively charged ion, and wherein the amount of each reagent has following mol ratio:
YO 2/X 2O 3 50/1~∞
OH -/YO 2 0.15/1~0.7/1
Q/YO 2 0.1/1~0.5/1
H 2O/YO 2 20/1~60/1
M +/YO 2 0.05/1~0.20/1
The solution that obtains in (a) was reacted 3-28 days down at 150-180 ℃, generate the solid crystal material;
(c) be no more than 170 ℃ of following drying solid crystalline materials, the crystalline material of this anhydrous form has the oxide molar of general formula (III) to form
YQ 2OmM 2/nOzX 2O 3YO 2(III) in the formula, y has 0.1~1 numerical value, and Q is the organic formwork agent of general formula (II), and M is basic metal and/or alkaline earth metal cation, and m, n, z, X and Y have the identical definition of stipulating above;
(d) crystalline material (III) that obtains in step (c) at 500-700 ℃ roasting temperature is 4-20 hour, and last
(e) use H +To small part replacement positively charged ion M, obtain the acid type ERS-10 zeolite of general formula (I).
6. according to the method for claim 5, it is characterized in that, in step (a), can be hydrolyzed into X 2O 3Compound be selected from aluminium isopropylate, Tai-Ace S 150, NaAlO 2
7. according to the method for claim 6, wherein aluminum compound is selected from aluminium isopropylate and Tai-Ace S 150.
8. according to the method for claim 5, it is characterized in that, in step (a), can be hydrolyzed into YO 2Compound be the silicon compound that is selected from tetraethyl orthosilicate, colloidal silica, water glass, the silicon oxide of igniting.
9. method according to Claim 8 is characterized in that, silicon compound is selected from tetraethyl orthosilicate, colloidal silica.
10. according to the method for claim 5, it is characterized in that cationic source is sodium hydroxide or potassium hydroxide.
11. the method according to claim 5 is characterized in that, organic formwork agent (Q) is for there being the compound of formula (II), and wherein n is identical with n ', all is 5, X -Be OH -
12. the method according to claim 5 is characterized in that, the quantity of each component of solution has following mol ratio:
SiO 2/X 2O 3 80/1~∞
OH -/SiO 2 0.2/1~0.45/1
Q/SiO 2 0.2/1~0.3/1
H 2O/SiO 2 40/1~50/1
M +/SiO 2 0.09/1~0.15/1
13. the method according to claim 5 is characterized in that, temperature of reaction is about 170 ℃, and the reaction times is 7~14 days.
14. the method according to claim 5 is characterized in that, described drying is carried out under 90~120 ℃.
15. the method according to claim 5 is characterized in that, roasting was carried out under 550~650 ℃ 6~15 hours.
16. the method according to claim 5 is characterized in that, in step (e), replaces with mineral acid or ammonium salt ion-exchange.
17. according to the method for claim 16, wherein said mineral acid is a hydrochloric acid.
18. according to the method for claim 16, wherein said ammonium salt is an ammonium acetate.
19. zeolite precursor that its anhydrous form has general formula (III) oxide molar to form
YQ 2OmM 2/nOzX 2O 3YO 2(III) in the formula, y has 0.1~1 numerical value, and Q is for there being the organic formwork agent of general formula (II) In the formula, n and n ' are identical or different, are an integer in 3~6, X -For being selected from OH -, muriate, bromide, fluorochemical and iodide negatively charged ion, M is that valence mumber is basic metal or the alkaline earth metal cation of n, z is the number in 0~0.02, X represents to be selected from one or more elements in aluminium, iron, gallium, boron, vanadium, arsenic, antimony, chromium and the manganese, Y represents to be selected from one or more elements in silicon, germanium, titanium, the zirconium, and this zeolite precursor is represented with the X-ray powder diffraction figure shown in the following table 2:
Table 2d () I/I 010011.1±0.1 s6.82±0.08 w5.83±0.06 w4.64±0.05 m4.32±0.05 vs4.00±0.04 s3.72±0.03 m3.42±0.03 w3.35±0.03 w3.27±0.02 m3.08±0.02 w2.70±0.01 w2.58±0.01 w2.54±0.01 w2.39±0.01 w2.32±0.01 w2.29±0.01 w2.12±0.01 w2.11±0.01 w1.94±0.01 w
20. claim 1~4 each porous crystalline material ERS-10 or each the porous crystalline material ERS-10 of method preparation of claim 5-18 as molecular sieve, ion-exchanger and the purposes in hydrocarbon conversion catalytic process.
CN97103349A 1996-03-21 1997-03-20 ERS-10 zeolite and process for its preparation Expired - Fee Related CN1104284C (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
IT000556A/96 1996-03-21
IT000556A/1996 1996-03-21
IT96MI000556A IT1283284B1 (en) 1996-03-21 1996-03-21 ZEOLITE ERS-10 AND PROCEDURE FOR ITS PREPARATION

Publications (2)

Publication Number Publication Date
CN1164439A CN1164439A (en) 1997-11-12
CN1104284C true CN1104284C (en) 2003-04-02

Family

ID=11373723

Family Applications (1)

Application Number Title Priority Date Filing Date
CN97103349A Expired - Fee Related CN1104284C (en) 1996-03-21 1997-03-20 ERS-10 zeolite and process for its preparation

Country Status (12)

Country Link
US (1) US5910299A (en)
EP (1) EP0796821B1 (en)
JP (1) JPH111319A (en)
CN (1) CN1104284C (en)
AT (1) ATE183987T1 (en)
DE (1) DE69700457T2 (en)
DK (1) DK0796821T3 (en)
EA (1) EA000242B1 (en)
ES (1) ES2135960T3 (en)
GR (1) GR3031380T3 (en)
IT (1) IT1283284B1 (en)
SI (1) SI0796821T1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104870368A (en) * 2012-12-18 2015-08-26 环球油品公司 Hydrocarbon processes using UZM-43 an EUO-NES-NON zeolite
CN104870368B (en) * 2012-12-18 2016-11-30 环球油品公司 Use UZM-43, the hydroconversion process of a kind of EUO-NES-NON zeolite

Families Citing this family (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5670131A (en) * 1995-10-02 1997-09-23 Mobil Oil Corporation Synthetic porous crystalline MCM-61, its synthesis and use
WO1998029337A1 (en) * 1996-12-31 1998-07-09 Chevron U.S.A. Inc. Zeolite ssz-47
IT1299035B1 (en) * 1998-04-07 2000-02-07 Enichem Spa PROCESS FOR THE PREPARATION OF MONOALKYLATED AROMATIC COMPOUNDS
IT1304792B1 (en) 1998-12-22 2001-03-29 Agip Petroli CATALYTIC COMPOSITION FOR THE UPGRADING OF HYDROCARBONS WITH POINT BOILING IN THE NAFTA INTERVAL.
ES2155761B1 (en) * 1998-12-22 2001-12-01 Univ Valencia Politecnica ZEOLITA ITQ-7.
US20100291334A1 (en) * 2002-12-27 2010-11-18 Univation Technologies, Llc Broad Molecular Weight Polyethylene Having Improved Properties
US6989344B2 (en) * 2002-12-27 2006-01-24 Univation Technologies, Llc Supported chromium oxide catalyst for the production of broad molecular weight polyethylene
US20050084446A1 (en) * 2003-10-17 2005-04-21 Schmitt Kirk D. Zeolite synthesis with directing agents with approximately perpendicular groups
CN1314588C (en) * 2004-12-28 2007-05-09 华东师范大学 Titanium-silicon molecular screen ECNU-2 and synthesizing method thereof
CN1328164C (en) * 2004-12-28 2007-07-25 华东师范大学 Molecular screen ECNU-3 and synthesizing method thereof
ES2263369B1 (en) * 2005-02-02 2007-12-16 Universidad Politecnica De Valencia MICROPOROUS CRYSTAL MATERIAL OF ZEOLITIC NATURE, ZEOLITA ITQ-32, PREPARATION AND USE PROCEDURE.
FR2882744B1 (en) * 2005-03-07 2008-06-06 Inst Francais Du Petrole COK-7 CRYSTALLIZED SOLID, PROCESS FOR THE PREPARATION AND USE FOR THE PROCESSING OF HYDROCARBONS
ITMI20061231A1 (en) * 2006-06-26 2007-12-27 Eni Spa PROXCESS AND ZEOLITHIC MATERIALS FOR GAS SEPARATION
ITMI20081036A1 (en) * 2008-06-06 2009-12-07 Eni Spa CRACKING PROCESS AND IMPROVED CATALYSTS FOR SUCH PROCESS
IT1392806B1 (en) * 2009-02-02 2012-03-23 Eni Spa FLUID BED INTEGRATED CATALYTIC CRACKING PROCESS TO OBTAIN HYDROCARBURIC MIXTURES WITH HIGH QUALITY AS FUEL
EP3246287A1 (en) 2011-02-11 2017-11-22 ZS Pharma, Inc Microporous zirconium silicate for the treatment of hyperkalemia
US9943637B2 (en) 2012-06-11 2018-04-17 ZS Pharma, Inc. Microporous zirconium silicate and its method of production
CA2878832A1 (en) 2012-07-11 2014-01-16 ZS Pharma, Inc. Microporous zirconium silicate for the treatment of hyperkalemia in hypercalcemic patients and improved calcium-containing compositions for the treatment of hyperkalemia
US10695365B2 (en) 2012-10-22 2020-06-30 ZS Pharma, Inc. Microporous zirconium silicate for the treatment of hyperkalemia
AU2013334776B2 (en) 2012-10-22 2017-08-31 ZS Pharma, Inc. Microporous zirconium silicate for treating hyperkalemia
US8916129B2 (en) * 2012-12-18 2014-12-23 Uop Llc UZM-43 an EUO-NES-NON zeolite
US9592253B1 (en) 2015-10-14 2017-03-14 ZS Pharma, Inc. Extended use zirconium silicate compositions and methods of use thereof
CN112174163B (en) * 2020-09-22 2022-03-29 嘉兴学院 Method for synthesizing ERS-10 zeolite by solvent-free route

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5102641A (en) * 1988-12-22 1992-04-07 Imperial Chemical Industries Plc Zeolite nu-87
US5246690A (en) * 1985-12-19 1993-09-21 Eniricerche S.P.A. Synthetic, crystalline, porous material containing silicon oxide, titanium oxide and aluminum oxide
US5385718A (en) * 1990-06-21 1995-01-31 Imperial Chemical Industries Plc Zeolites
US5645812A (en) * 1993-10-01 1997-07-08 Chevron U.S.A. Inc. Zeolite ZSM-11 and a process for preparing zeolite ZSM-11 using a 3,5-dimethylpiperidinium templating agent

Family Cites Families (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3165380D1 (en) * 1980-06-12 1984-09-13 Ici Plc Zeolite eu-1
EP0063436B1 (en) * 1981-04-14 1986-12-30 Imperial Chemical Industries Plc Zeolites
US4508837A (en) * 1982-09-28 1985-04-02 Chevron Research Company Zeolite SSZ-16
US4610854A (en) * 1982-10-29 1986-09-09 Chevron Research Company Zeolite SSZ-15 and process for preparing the same
US4568654A (en) * 1982-11-03 1986-02-04 Mobil Oil Corporation Zeolite ZSM-51 composition
GB8318336D0 (en) * 1983-07-06 1983-08-10 Ici Plc Zeolites
US4640829A (en) * 1984-04-16 1987-02-03 Mobil Oil Corporation Synthesis of crystalline silicate ZSM-50 using dibenzyldimethylammonium ions and the product produced
SU1188096A1 (en) * 1984-05-18 1985-10-30 Bruss Ti Kirova Method of producing alumophosphate of zeolite structure
SU1614757A3 (en) * 1985-12-09 1990-12-15 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. (Фирма) Method of producing ferrierite
US5290533A (en) * 1985-12-19 1994-03-01 Eniricerche S.P.A. Method for production of a coated substrate with controlled surface characteristics
RU1610777C (en) * 1988-01-20 1995-06-27 Всесоюзный научно-исследовательский институт по переработке нефти Method of preparing high-silicon zeolite type zsm-5
US5252527A (en) * 1988-03-23 1993-10-12 Chevron Research And Technology Company Zeolite SSZ-32
US5106801A (en) * 1988-10-20 1992-04-21 Chevron Research And Technology Company Zeolite SSZ-31
SU1745678A1 (en) * 1990-02-21 1992-07-07 Институт Химии Силикатов Им.И.В.Гребенщикова Process for producing zeolite zsm-11
US5425933A (en) * 1992-06-30 1995-06-20 Chevron Research And Technology Company, A Division Of Chevron U.S.A. Inc. Method for preparing crystalline materials using heterobridged aza-polycyclic templating agents
US5268161A (en) * 1992-10-09 1993-12-07 Chevron Research And Technology Company Process for preparing molecular sieves using a 1,3,3,8,8-pentamethyl-3-azoniabicyclo [3.2.1] octane template
US5271921A (en) * 1992-10-09 1993-12-21 Chevron Research And Technology Company Process for preparing molecular sieves using 3,7-diazabicyclo[3.3.1]
ES2139752T3 (en) * 1993-10-18 2000-02-16 Mobil Oil Corp SYNTHETIC POROUS CRYSTAL MATERIAL, MCM-58, ITS SYNTHESIS AND USE.
AU2549295A (en) * 1995-03-17 1996-10-08 Chevron U.S.A. Inc. Preparation of zeolites using organic template and amine

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5246690A (en) * 1985-12-19 1993-09-21 Eniricerche S.P.A. Synthetic, crystalline, porous material containing silicon oxide, titanium oxide and aluminum oxide
US5102641A (en) * 1988-12-22 1992-04-07 Imperial Chemical Industries Plc Zeolite nu-87
US5385718A (en) * 1990-06-21 1995-01-31 Imperial Chemical Industries Plc Zeolites
US5645812A (en) * 1993-10-01 1997-07-08 Chevron U.S.A. Inc. Zeolite ZSM-11 and a process for preparing zeolite ZSM-11 using a 3,5-dimethylpiperidinium templating agent

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104870368A (en) * 2012-12-18 2015-08-26 环球油品公司 Hydrocarbon processes using UZM-43 an EUO-NES-NON zeolite
CN104870368B (en) * 2012-12-18 2016-11-30 环球油品公司 Use UZM-43, the hydroconversion process of a kind of EUO-NES-NON zeolite

Also Published As

Publication number Publication date
IT1283284B1 (en) 1998-04-16
EA000242B1 (en) 1999-02-25
US5910299A (en) 1999-06-08
ITMI960556A0 (en) 1996-03-21
ITMI960556A1 (en) 1997-09-21
EP0796821A1 (en) 1997-09-24
SI0796821T1 (en) 2000-02-29
EA199700027A1 (en) 1997-09-30
JPH111319A (en) 1999-01-06
GR3031380T3 (en) 2000-01-31
DK0796821T3 (en) 2000-01-24
ES2135960T3 (en) 1999-11-01
DE69700457D1 (en) 1999-10-07
CN1164439A (en) 1997-11-12
ATE183987T1 (en) 1999-09-15
EP0796821B1 (en) 1999-09-01
DE69700457T2 (en) 2000-03-30

Similar Documents

Publication Publication Date Title
CN1104284C (en) ERS-10 zeolite and process for its preparation
CN1313372C (en) Crystalline aluminosilicate zeolitic composition: UZM-4M
CN1016773B (en) The layered silicate preparation method
CN1048001C (en) ZSM-5 zeolite
CN1180978C (en) Microporous crystalline silico-alumino-phosphate composition, catalytic material comprising said composition and use thereof
CN86108842A (en) The method of dewaxing catalyst and use titanoaluminosilicatmolecular molecular sieves
CN1185779A (en) A process for preparing zeolites having MTT crystal structure using small, natural amines
CN1073411A (en) In reaction mixture, use the method for diethanolamine synthesizing zeolite-betafite
CN1006445B (en) Catalytic cracking catalyst and its preparation method
CN106795001A (en) The method for preparing zeolite SSZ 52 using the structure directing agent for calculating prediction
JP2021524431A (en) Method for synthesizing high-purity AFX-structured zeolite in the presence of organic nitrogen-containing structuring agent
CN1018624B (en) Crystalline aluminumphosphate compostions
CN1226875A (en) Preparation of Y-type faujasite using organic template
CN1181744A (en) Process for preparing medium pore size zeolites using neutral amines
CN1093514C (en) Large crystal ZSM-5, its synthesis and use
CN1007067B (en) Catalytic cracking process for producing high octane gasoline products
JP2010260777A (en) Method for producing phosphorus-containing beta type zeolite
CN1085618C (en) Magnesiosilicates
CN1016678B (en) Crystalline silicate ZSM-11 is synthetic
CN1856361A (en) Molecular sieve SSZ-61 composition of a matter and synthesis thereof
CN1022465C (en) Hydrocarbon cracking catalyst containing phosphorus
JP2021524432A (en) Method for producing high-purity AFX-structured zeolite using a nitrogen-containing organic structuring agent
CN1182914C (en) Zin-aluminium silicates with FAU structure
CN1270852A (en) Rare earth element containing molecular sieve and its preparation
CN1007879B (en) Cracking catalyst of clay molecular sieve with layer structure

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20030402

Termination date: 20120320